Christos Akratos

Prof. Dr. Christos Akratos

Depertment of Civil Engineering, Democritus University of Thrace
orcid

Research Focus & Metrics

Academic Career Length

21Years (2006-Present)

(Calculated once Scilit publication data is synced: current year − year of first publication + 1)

Representative Publications

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1 February 2007 in Ecological Engineering
Verified
Journal Article
Closed access
Christos AkratosChristos Akratos
Christos Akratos
VTVassilios A. Tsihrintzis
Vassilios A. Tsihrintzis

1 November 2013 in International Biodeterioration & Biodegradation
Verified
Journal Article
Closed access
ACAbu Khayer Md. Muktadirul Bari Chowdhury
Abu Khayer Md. Muktadirul Bari Chowdhury
Christos AkratosChristos Akratos
Christos Akratos
DVDimitrios V. Vayenas
Dimitrios V. Vayenas
SPStavros Pavlou
Stavros Pavlou

1 September 2008 in Chemical Engineering Journal
Verified
Journal Article
Closed access
Christos AkratosChristos Akratos
Christos Akratos
JPJohn N.E. Papaspyros
John N.E. Papaspyros
VTVassilios A. Tsihrintzis
Vassilios A. Tsihrintzis

14 January 2019 in Water
Verified
Journal Article
Open access
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AKAggelos Kotoulas
Aggelos Kotoulas
DADimitra Agathou
Dimitra Agathou
ITIrene E. Triantaphyllidou
Irene E. Triantaphyllidou
TTTriantafyllos Tatoulis
Triantafyllos Tatoulis
Christos AkratosChristos Akratos
Christos Akratos
Dimitris VayenasDimitris Vayenas
Dimitris Vayenas
The efficiency of natural zeolite to remove ammonium from artificial wastewater (ammonium aqueous solutions) and to treat second cheese whey was examined, aiming to recover nitrogen nutrients that can be used for further applications, such as slow-release fertilizers. Sorption experiments were performed using artificial wastewater and zeolite of different granulometries (i.e., 0.71–1.0, 1.8–2.0, 2.0–2.8, 2.8–4.0, and 4.0–5.0 mm). The granulometry of the zeolite had no significant effect on its ability to absorb ammonium. Nevertheless, smaller particles (0.71–1.0 mm) exhibited quicker NH4+-N adsorption rates of up to 93.0% in the first 10 min. Maximum ammonium removal efficiency by the zeolite was achieved at ammonium concentrations ranging from 10 to 80 mg/L. Kinetic experiments revealed that chemisorption is the mechanism behind the adsorption process of ammonium on zeolite, while the Freundlich isotherm model fitted the experimental data well. Column sorption experiments under batch operating mode were performed using artificial wastewater and second cheese whey. Column experiments with artificial wastewater showed high NH4+-N removal rates (over 96% in the first 120 min) for all granulometries and initial NH4+-N concentrations tested (200 and 5000 mg/L). Column experiments with second cheese whey revealed that natural zeolite can remove significant organic loads (up to 40%, 14.53 mg COD/g of zeolite) and NH4+-N (about 99%). For PO43−-P, the zeolite appeared to saturate after day 1 of the experiments at a removal capacity of 0.15 mg P/g of zeolite. Desorption experiments with water resulted in low NH4+-N and PO43−-P desorption rates indicating that the zeolite could be used as a substrate for slow nitrogen release in soils.

1 June 2007 in Environmental Technology
Verified
Journal Article
Closed access
VTV. A. Tsihrintzis
V. A. Tsihrintzis
Christos AkratosChristos Akratos
Christos Akratos
GGGeorgios D. Gikas
Georgios D. Gikas
DKD. Karamouzis
D. Karamouzis
AAA. N. Angelakis
A. N. Angelakis
The biodegradation of municipal solid waste (MSW) was investigated in simulated bioreactor landfills under aerobic conditions. The bioreactors were operated to determine Two constructed wetland systems, treating domestic wastewater, are compared in terms of performance and costs. One is a free water surface (FWS) wetland system located in Pompia, Crete, south Greece, and the other one is a vertical subsurface flow (VSF) wetland system located in Gomati, Chalkidiki, north Greece. The FWS system is designed for 1200 p.e. Its construction cost was [euro]305,000, and the capital, operation and maintenance cost was [euro]22.07 p.e.−1 yr−1 or [euro]0.50 m−3 of influent. The VSF system is designed for 1000 p.e. Its construction cost was [euro]410,850, and the capital, operation and maintenance cost was [euro]36.81 p.e.−1 yr−1 or [euro]0.56 m−3 of influent. Both systems achieved high removal rates for BOD5, COD, TSS, TKN, phosphorus, TC, and FC, which makes them ideal for small communities in the Mediterranean region.

1 June 2011 in Ecological Engineering
Verified
Journal Article
Closed access
EHElissavet Herouvim
Elissavet Herouvim
Christos AkratosChristos Akratos
Christos Akratos
Athanasia TekerlekopoulouAthanasia Tekerlekopoulou
Athanasia Tekerlekopoulou
DVDimitrios V. Vayenas
Dimitrios V. Vayenas